US2822320A - Reclaiming used lubricating oil - Google Patents

Reclaiming used lubricating oil Download PDF

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Publication number
US2822320A
US2822320A US612891A US61289156A US2822320A US 2822320 A US2822320 A US 2822320A US 612891 A US612891 A US 612891A US 61289156 A US61289156 A US 61289156A US 2822320 A US2822320 A US 2822320A
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Prior art keywords
oil
hydrazine
lubricating oil
used lubricating
impurities
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US612891A
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Mitacek Bill
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Phillips Petroleum Co
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Phillips Petroleum Co
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M175/00Working-up used lubricants to recover useful products ; Cleaning
    • C10M175/0016Working-up used lubricants to recover useful products ; Cleaning with the use of chemical agents

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Lubricants (AREA)

Description

RECLAIMING USED LUBRICATING OIL Bill Mitacek, Bartlesviile, Okla, assignor to Phillips Petroleum Company, a corporation of Delaware No Drawing. Application September 28, 1956 Serial No. 612,891
4 Claims. (Cl. 196-16) This invention relates ot a method for purification of used lubricating oils. In one aspect it relates to a method S tes ate Patented Feb. 1958 2 vices designed to provide thorough mixingxof the contents. The separation of the oil phase from the sludge phase, which is produced by the treatment, can be effected either by gravity, such as an ordinary settling tank'or a rotary stratifier, or by centrifuges, or the like.
When desired, the lubricating oil can be clay treated as a first step of treatment, in order to remove part of the impurities, and can also be given a final clay treatment in order to improve the color of the reclaimed oil prior toreuse. Either or both of the clay-treated steps can be eliminated if desired.
for removing dissolved impurities and dispersed insoluble 2";
impurities from mineral oils. 1 V i It is known to treat used lubricating oils to remove impurities introduced therein in the use of such oils. It is common knowledge that lubricating oils in use become contaminated with solid materials such as rust and carbon and with dissolved or suspended sludge and acidic materials. It is also known to those skilled in the art that the contaminated lubricating oil can be processed to obtain therefrom a purified lubricating oil which can satisfactorily be used for further service in engine crank cases. The methods of the prior art have not been altogether satisfactory because of the requirement for conducting the purification at elevated temperatures, and because of other disadvantages.
It is therefore an object of this invention to provide a method for the removal of impurities from used lubricating oils in Which the use of high temperature is not required. It is also an object of this invention to pro vide an agent for the treatment of used lubricating oils which exhibits limited but appreciable solubility in the lubricating oil, thereby providing improved contact between the treating agent and the impurities in the oil. It is a further object of this invention to provide a method for the purification of used lubricating oils with an inorganic treating agent wherein water is not formed in the purification reaction. Further objects and advantages of this invention will become apparent to one skilled in the art upon study of the the present disclosure.
This invention comprises a process for reclaiming lubricating oils which have been used in internal combustion engines by addition of a small quantity of hydrazine resulting in precipitation of the impurities as a sludge phase. The precipitation step is then followed by separation of the sludge phase and recovery of the oil phase. The recovered oil phase can be washed to remove dissolved hydrazine or can be heated to vaporize the hydrazine and can be clay treated for color improvement prior to reuse when desired.
The process of reclaiming lubricating oil can be practiced by contacting the oil with about 0.5 to about 10 volume percent or more of hydrazine (based on vol. of oil) providing suflicient agitation to the mixture to ensure adequate contact of the hydrazine with the impurities in the oil, separating the sludge which is formed, by settling, centrifuging or similar process, and recovering the oil phase for further use. The contacting of used oil and hydrazine can be carried out at temperatures preferably in the range of 50 to 150 F. although higher and lower temperatures can be used if desired. Atmospheric pressure is usually preferred although the purification treatment can be carried out at sub-atmospheric pressures or at super-atmospheric pressures if desired. The treatment can be carried out in many types of equipment, for example, centrifugal pumps, agitated tanks, and similar de- It is also within the concept of this invention to water: wash the oil phase recovered from the process to remove dissolved hydrazine which may remain in the treated oil, or removal of the hydrazine can be elfected by washing with a dilute acid followed by a water wash. Hydrazine can also be removed by distillation.
The following example illustrates a specific embodiment of the invention, but is not to be construed as limiting the example. i
An engine test has been devised to produce maximum sludging in an engine crankcase. In this test the engine is operated in six hour cycles according to the schedule shown in the following Table I.
A 96 hour test will comprise 16 operating cycles. The test is usually referred to as a cold engine sludge test.
EXAMPLE A used oil sample was obtained from :a 96-hour cold engine sludge test as described above and was divided into three portions. One portion was treated with 5 volume percent hydrazine, the second with 10 volume percent hydrazine, and the third sample was not treated. Table II contains analytical data obtained on each of these portions and on the original (new) oil prior to the engine test. The new oil was a dewaxed-solvent extracted paraffin base lubricating oil containing 0.75 percent Lubrizol 309 (trade mark) available from the Lubrizol Corporation and be-' lieved to comprise an ester of zine dithiophosphate and a small amount of barium sulfonate.
TABLE II Treatment 0 used lube oil with hydrazine Used 011 from Engine Test (96 hours) New 011 Hydrazine Treated With- Untreated 10 Vol. 5 Vol. Percent Percent Vls. at 100 F., SUS 518. 8 665. 5 422. 9 429.8 Vls. at 210 F SUS 64. 87 69. 61 60.0 V. I 99 99 99 0. 21 0. 48 0. 12 0. 12 Ramsbottom 0 Res 0. 24 6.98 0. 32 0.39 0.23 1.86 0.09 0.12 NPA Color 8 8 API Grav 27. 6 27.3 Naphtha Insol- 0. 03 0. 06 OHOla Insol Pour Point, F
..It will be noted that hydrazine treatment resulted in lower carbon residue, ash, and naphtha insolubles in comparison with the untreated used oil. The used oil contained a consider'ablefamount of sludge whichwas pre cipitated by'thelhydra'zine. V
Reasonable variations and modifications are possible within the scope of the disclosure of this invention, the essence of which is the discovery that hydrazine can be utilized as a treating agent in reclaiming used lubricating oils at ordinary temperatures and pressures.
.That which is claimed is:
1. A process for removing impurities from used lubricating oil which comprisesintimately admixing hydrazine with said oil; and recovering purified lubricating oil as a product of the process.
2. A process for removing dispersed impurities from used lubricating oil which comprises intimately admixing hydrazinewith said oil in an amount in the range of 0.5 to 10 volume percent with said oil; separating and removing resulting precipitate therefrom; washing the resulting oil with water and recovering purified oil therefrom as a product of the process.
3. A process for removing dispersed impurities from 4 used lubricating oil which comprises intimately admixing hydrazine with said oil in an amount of 0.5 to 5 volume percent of said oil; separating resulting precipitate there from; washing the resulting oil with water; contacting the water-washed oil with a sufficient amount of clay to prove the color of the oil; and recovering a purified oil therefrom as the product of the' process.
4. A process for removing dispersed impurities from used lubricating oil which comprises contacting said oil with finely divided clay; separating said oil from said clay; intimately admixing hydrazine with said oil in an amount of 0.5 to 5 volume percent of said oil; separating and removing a resulting precipitate therefrom; water-washing the resulting oil; contacting said water-washed oil with a sufficient amount of finely divided clay to improve the color of said oil; and recovering said oil from said clay as the product of the process.
References Cited in the file of this patent UNITED STATES PATENTS 1,849,654 Baylis Mar. 15, ,1932 2,368,596 Johnston et al Jan. 30, .1945 2,393,335 Musselman Jan. 22, 1946

Claims (2)

1. A PROCESS FOR REMOVING IMPURITIES FROM USED LUBRICATING OIL WHICH COMPRISES INTIMATELY ADMIXING HYDRAZINE WITH SAID OIL; AND RECOVERING ADMIXING HYDRAZINE PRODUCT OF THE PROCESS.
3. A PROCESS FOR REMOVING DISPERSED IMPURITIES FROM USED LUBRICATING OIL WHICH COMPRISES INTIMATELY ADMIXING HYDRAZINE WITH SAID OIL IN AN AMOUNT OF 0.5 TO 5 VOLUME PERCENT OF SAID OIL; SEPARATING RESULTING PRECIPITATE THEREFROM, WASHING THE RESULTING OIL WITH WATER, CONTACTING THE WATER-WASHED OIL WITH A SUFFICIENT AMOUNT OF CLAY TO IMPROVE THE COLOR OF THE OIL; AND RECOVERING A PURIFIED OIL THEREFROM AS THE PRODUCT OF THE PROCESS.
US612891A 1956-09-28 1956-09-28 Reclaiming used lubricating oil Expired - Lifetime US2822320A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3305478A (en) * 1964-08-13 1967-02-21 Dow Chemical Co Process for re-refining used lubricating oils
WO1990007566A1 (en) * 1989-01-04 1990-07-12 Geut Ag Gesellschaft Für Energie Und Umwelttechnik Process for reprocessing waste oil
TR26396A (en) * 1989-04-20 1995-03-15 Thomson Comsumer Electronics I TELEVISION RECEIVER AS AUXILIARY INPUT CONNECTOR FOR VIDEO SIGNALS OF A SEPARATED Y-C FORMAT
WO2008032129A1 (en) * 2006-09-14 2008-03-20 David Tamas Improved method for purifying contaminated oils

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1849654A (en) * 1926-10-14 1932-03-15 Filtrol Company Method of reclaiming used lubricating oils
US2368596A (en) * 1943-03-16 1945-01-30 Shell Dev Process for removing dispersed friedel-crafts sludge
US2393335A (en) * 1942-10-29 1946-01-22 Standard Oil Co Reclaiming used lubricating oils

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1849654A (en) * 1926-10-14 1932-03-15 Filtrol Company Method of reclaiming used lubricating oils
US2393335A (en) * 1942-10-29 1946-01-22 Standard Oil Co Reclaiming used lubricating oils
US2368596A (en) * 1943-03-16 1945-01-30 Shell Dev Process for removing dispersed friedel-crafts sludge

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3305478A (en) * 1964-08-13 1967-02-21 Dow Chemical Co Process for re-refining used lubricating oils
WO1990007566A1 (en) * 1989-01-04 1990-07-12 Geut Ag Gesellschaft Für Energie Und Umwelttechnik Process for reprocessing waste oil
TR26396A (en) * 1989-04-20 1995-03-15 Thomson Comsumer Electronics I TELEVISION RECEIVER AS AUXILIARY INPUT CONNECTOR FOR VIDEO SIGNALS OF A SEPARATED Y-C FORMAT
WO2008032129A1 (en) * 2006-09-14 2008-03-20 David Tamas Improved method for purifying contaminated oils

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